Absorbent Article Comprising A Synthetic Polymer Derived from A Renewable Resource and Methods of Producing Said Article

ABSTRACT

A method for making a disposable absorbent article is provided. The method comprises the steps of providing a first nonwoven comprising synthetic fibers comprising a 14C/C ratio of about 1.0×10−14 or greater, providing a second nonwoven comprising synthetic fibers comprising a comprising a 14C/C ratio of about 1.0×10−14 or greater, converting the second nonwoven into a topsheet so that the topsheet comprises a Liquid Strike Through value of less than 4 seconds, and combining the first nonwoven and the topsheet with other absorbent article components to form a disposable absorbent article.

CROSS REFERENCE TO RELATED APPLICATION

This application is a continuation of U.S. patent application Ser. No.17/203,870, filed on Mar. 17, 2021, which is a continuation of U.S.patent application Ser. No. 17/144,484, filed on Jan. 8, 2021, nowgranted U.S. Pat. No. 11,186,976, which is a continuation of U.S. patentapplication Ser. No. 16/667,969, filed on Oct. 30, 2019, now grantedU.S. Pat. No. 10,920,407, which is a continuation of U.S. patentapplication Ser. No. 16/194,670, filed on Nov. 19, 2018, now grantedU.S. Pat. No. 10,501,920, which is a continuation of U.S. patentapplication Ser. No. 15/011,930, filed on Feb. 1, 2016, now granted U.S.Pat. No. 10,166,312, which is a continuation of U.S. patent applicationSer. No. 12/975,914, filed on Dec. 22, 2010, now abandoned, which is acontinuation of U.S. patent application Ser. No. 11/724,341, filed onMar. 15, 2007, now abandoned, and which claims the benefit of U.S.Provisional Patent Application No. 60/783,274, filed on Mar. 17, 2006,the entire disclosures of all of which are hereby incorporated byreference herein.

FIELD OF INVENTION

The present invention relates to an absorbent article which comprisessynthetic polymeric materials derived from renewable resources, wherethe materials have specific performance characteristics making themparticularly useful in said absorbent article.

BACKGROUND OF THE INVENTION

Furthermore, many consumers display an aversion to purchasing productsthat are derived from petrochemicals. In some instances, consumers arehesitant to purchase products made from limited non-renewable resourcessuch as petroleum and coal. Other consumers may have adverse perceptionsabout products derived from petrochemicals being “unnatural” or notenvironmentally friendly.

Certain alternative materials which are derived from non-petrochemicalor renewable resources have been disclosed for use in absorbentarticles. For example, U.S. Pat. No. 5,889,072 to Chao describes aprocess for preparing a cross-linked polyaspartate superabsorbentmaterial. U.S. Pat. Nos. 6,713,460 and 6,444,653, both to Huppe et al.,describe a superabsorbent material comprising glass-likepolysaccharides. Furthermore, diapers having varying degrees ofbiodegradability have been disclosed. U.S. Pat. No. 5,783,504 to Ehretet al. describes a composite structure, which is suitable for use indiapers, comprising a nonwoven manufactured from a polymer derived fromlactic acid and a film manufactured from a biodegradable aliphaticpolyester polymer. PCT application WO 99/33420 discloses asuperabsorbent material comprising a renewable and/or biodegradable rawmaterial. However, these diapers and materials tend to havesignificantly lower performance and/or higher cost than materialsderived from petrochemicals. For example, the superabsorbent materialsdisclosed in WO 99/33420 show a low absorption capacity under load and alow gel strength. A superabsorbent material with low gel strength tendsto deform upon swelling and reduce interstitial spaces between thesuperabsorbent particles. This phenomenon is known as gel-blocking. Oncegel-blocking occurs, further liquid uptake or distribution takes placevia a very slow diffusion process. In practical terms, gel-blockingincreases the susceptibility of the absorbent article to leakage.

Accordingly, it would be desirable to provide an absorbent article whichcomprises a polymer derived from renewable resources, where the polymerhas specific performance characteristics making the polymer particularlyuseful in the absorbent article. Ideally, it would be desirable toprovide a consumer product including a plurality of absorbent articlescomprising said polymer derived from renewable resources and acommunication of a related environmental message.

SUMMARY OF THE INVENTION

The present invention relates to an absorbent article having opposinglongitudinal edges, the absorbent article comprising a topsheet, abacksheet joined with the topsheet, an absorbent core disposed betweenthe topsheet and the backsheet, and a synthetic polymer derived from afirst renewable resource via at least one monomeric intermediatecompound. The polymer is disposed in or incorporated into one or moreelements of the absorbent article. The elements are selected from agroup consisting of the absorbent core, the topsheet, the backsheet, anda barrier leg cuff.

The present invention further relates to an absorbent article having abody-facing surface, and a garment-facing surface. The article comprisesa topsheet, a backsheet joined with the topsheet, an absorbent coredisposed between the topsheet and the backsheet, a pair of barriercuffs, and a synthetic polyolefin. The synthetic polyolefin is derivedfrom a first renewable resource via at least one intermediate compound.The synthetic polyolefin is either polypropylene or polyethylene. Thetopsheet, backsheet, or cuff substrate comprises the polyolefin.

The present invention also relates to a method for making an absorbentarticle comprising the steps of providing a renewable resource, derivingan intermediate monomeric compound from the renewable resource,polymerizing the monomeric compound to form a synthetic polymer, anddisposing or incorporating the polymer into one or more elements of theabsorbent article. The elements are selected from a group consisting ofthe absorbent core, the topsheet, the backsheet, and a barrier leg cuff.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1A is a plan view of an exemplary absorbent article in the form ofa diaper in a flat, uncontracted state.

FIG. 1B is a cross-sectional view of the diaper of FIG. 1A taken alongthe lateral centerline.

FIGS. 2A-B are perspective views of a package comprising an absorbentarticle.

FIGS. 3A-F are illustrations of several suitable embodiments of iconscommunicating reduced petrochemical dependence and/or environmentalfriendliness.

FIG. 4 is a partial cross-sectional side view of a suitable permeabilitymeasurement system for conducting the Saline Flow Conductivity Test.

FIG. 5 is a cross-sectional side view of a piston/cylinder assembly foruse in conducting the Saline Flow Conductivity Test.

FIG. 6 is a top view of a piston head suitable for use in thepiston/cylinder assembly shown in FIG. 5.

FIG. 7 is a cross-sectional side view of the piston/cylinder assembly ofFIG. 5 placed on a fritted disc for the swelling phase.

DETAILED DESCRIPTION OF THE INVENTION

The present invention relates to an absorbent article comprising asynthetic polymer derived from a renewable resource where the polymerhas specific performance characteristics. When the synthetic polymerderived from a renewable resource is in the form of a superabsorbentpolymer, it exhibits an Absorption Against Pressure (AAP) value of atleast about 15.0 g saline per gram polymer and/or a saline flowconductivity (SFC) of at least about 30×10⁻⁷ cm³·sec/g. When the polymeris a polyolefin nonwoven suitable for use as a topsheet, it may exhibita Liquid Strike Through value of less than about 4 seconds. When thepolymer is a polyolefin nonwoven suitable for use as a barrier leg cuff,it may exhibit a hydrohead of at least about 5 mbar. When the polymer isa breathable polyolefin film suitable for use as a backsheet, it mayexhibit a Moisture Vapor Transmission Rate of at least about 2000g/m²/24 hr. When the polymer is a polyolefin film suitable for use as abacksheet, it may have an MD tensile strength of at least about 0.5N/cm.

In another aspect, the absorbent article comprises a synthetic polymerderived from a renewable resource wherein the polymer has a ¹⁴C/C ratioof about 1.0×10⁻¹⁴ or greater

The present invention further relates to a package comprising at leastone absorbent article comprising a synthetic polymer derived from arenewable resource and an overwrap securing the absorbent article(s).The absorbent article comprises a synthetic polymer derived from arenewable resource. The package may further comprise a communication ofa related environmental message.

The present invention further relates to a method for making absorbentarticles comprising a synthetic polymer derived from a renewableresource. The method comprises the following steps: providing arenewable resource; deriving at least one intermediate compound from therenewable resource, wherein the intermediate compound comprises amonomeric compound; polymerizing the monomeric compound to form at leastone polymer, wherein the at least one polymer exhibits the requisiteperformance for use in an absorbent article; and incorporating the atleast one polymer into an absorbent article. Additional steps, asdescribed herein, may be incorporated into the method. Optionally the atleast one polymer may be modified after the polymerization step.

I. Definitions

As used herein, the following terms shall have the meaning specifiedthereafter:

“Disposable” refers to items that are intended to be discarded after alimited number of uses, frequently a single use (i.e., the originalabsorbent article as a whole is not intended to be laundered or reusedas an absorbent article, although certain materials or portions of theabsorbent article may be recycled, reused, or composted). For example,certain disposable absorbent articles may be temporarily restored tosubstantially full functionality through the use ofremovable/replaceable components but the article is neverthelessconsidered to be disposable because the entire article is intended to bediscarded after a limited number of uses.

“Absorbent article” refers to devices which absorb and contain bodyexudates and, more specifically, refers to devices which are placedagainst or in proximity to the body of the wearer to absorb and containthe various exudates discharged from the body. Exemplary absorbentarticles include diapers, training pants, pull-on pant-type diapers(i.e., a diaper having a pre-formed waist opening and leg openings suchas illustrated in U.S. Pat. No. 6,120,487), refastenable diapers orpant-type diapers, incontinence briefs and undergarments, diaper holdersand liners, feminine hygiene garments such as panty liners (e.g. such asdisclosed in U.S. Pat. Nos. 4,425,130; 4,687,478; 5,267,992; and5,733,274), absorbent inserts, and the like. Absorbent articles may bedisposable or may contain portions that can be reused or restored.

“Proximal” and “Distal” refer, respectively, to the location of anelement relatively near to or far from the longitudinal or lateralcenterline of a structure (e.g., the proximal edge of a longitudinallyextending element is located nearer to the longitudinal centerline thanthe distal edge of the same element is located relative to the samelongitudinal centerline).

“Body-facing” and “garment-facing” refer respectively to the relativelocation of an element or a surface of an element or group of elements.“Body-facing” implies the element or surface is nearer to the wearerduring wear than some other element or surface. “Garment-facing” impliesthe element or surface is more remote from the wearer during wear thansome other element or surface (i.e., element or surface is proximate tothe wearer's garments that may be worn over the absorbent article).

“Superabsorbent” refers to a material capable of absorbing at least tentimes its dry weight of a 0.9% saline solution at 25° C. Superabsorbentpolymers absorb fluid via an osmotic mechanism to form a gel, oftenreferred to as, and used interchangeably with the term “hydrogel”.

“Longitudinal” refers to a direction running substantially perpendicularfrom a waist edge to an opposing waist edge of the article and generallyparallel to the maximum linear dimension of the article. Directionswithin 45 degrees of the longitudinal direction are considered to be“longitudinal”

“Lateral” refers to a direction running from a longitudinal edge to anopposing longitudinal edge of the article and generally at a right angleto the longitudinal direction. Directions within 45 degrees of thelateral direction are considered to be “lateral.”

“Disposed” refers to an element being located in a particular place orposition.

“Joined” refers to configurations whereby an element is directly securedto another element by affixing the element directly to the other elementand to configurations whereby an element is indirectly secured toanother element by affixing the element to intermediate member(s) whichin turn are affixed to the other element.

“Film” refers to a sheet-like material wherein the length and width ofthe material far exceed the thickness of the material. Typically, filmshave a thickness of about 0.5 mm or less.

“Impermeable” generally refers to articles and/or elements that are notpenetrative by fluid through the entire Z-directional thickness of thearticle under pressure of 0.14 lb/in² or less. Preferably, theimpermeable article or element is not penetrative by fluid underpressures of 0.5 lb/in² or less. More preferably, the impermeablearticle or element is not penetrative by fluid under pressures of 1.0lb/in² or less. The test method for determining impermeability conformsto Edana 120.1-18 or INDA IST 80.6.

“Extendibility” and “extensible” mean that the width or length of thecomponent in a relaxed state can be extended or increased by at leastabout 10% without breaking or rupturing when subjected to a tensileforce.

“Elastic,” “elastomer,” and “elastomeric” refer to a material whichgenerally is able to extend to a strain of at least 50% without breakingor rupturing, and is able to recover substantially to its originaldimensions after the deforming force has been removed.

“Elastomeric material” is a material exhibiting elastic properties.Elastomeric materials may include elastomeric films, scrims, nonwovens,and other sheet-like structures.

“Outboard” and “inboard” refer respectively to the location of anelement disposed relatively far from or near to the longitudinalcenterline of the diaper with respect to a second element. For example,if element A is outboard of element B, then element A is farther fromthe longitudinal centerline than is element B.

“Pant” refers to an absorbent article having a pre-formed waist and legopenings. A pant may be donned by inserting a wearer's legs into the legopenings and sliding the pant into position about the wearer's lowertorso. Pants are also commonly referred to as “closed diapers”,“prefastened diapers”, “pull-on diapers”, “training pants” and“diaper-pants.”

“Petrochemical” refers to an organic compound derived from petroleum,natural gas, or coal.

“Petroleum” refers to crude oil and its components of paraffinic,cycloparaffinic, and aromatic hydrocarbons. Crude oil may be obtainedfrom tar sands, bitumen fields, and oil shale.

“Renewable resource” refers to a natural resource that can bereplenished within a 100 year time frame. The resource may bereplenished naturally, or via agricultural techniques. Renewableresources include plants, animals, fish, bacteria, fungi, and forestryproducts. They may be naturally occurring, hybrids, or geneticallyengineered organisms. Natural resources such as crude oil, coal, andpeat which take longer than 100 years to form are not considered to berenewable resources

“Agricultural product” refers to a renewable resource resulting from thecultivation of land (e.g. a crop) or the husbandry of animals (includingfish).

“Monomeric compound” refers to an intermediate compound that may bepolymerized to yield a polymer.

“Polymer” refers to a macromolecule comprising repeat units where themacromolecule has a molecular weight of at least 1000 Daltons. Thepolymer may be a homopolymer, copolymer, terpoymer etc. The polymer maybe produced via fee-radical, condensation, anionic, cationic,Ziegler-Natta, metallocene, or ring-opening mechanisms. The polymer maybe linear, branched and/or crosslinked.

“Synthetic polymer” refers to a polymer which is produced from at leastone monomer by a chemical process. A synthetic polymer is not produceddirectly by a living organism.

“Polyethylene” and “polypropylene” refer to polymers prepared fromethylene and propylene, respectively. The polymer may be a homopolymer,or may contain up to about 10 mol % of repeat units from a co-monomer.

“Communication” refers to a medium or means by which information,teachings, or messages are transmitted.

“Related environmental message” refers to a message that conveys thebenefits or advantages of the absorbent article comprising a polymerderived from a renewable resource. Such benefits include being moreenvironmentally friendly, having reduced petroleum dependence, beingderived from renewable resources, and the like.

All percentages herein are by weight unless specified otherwise.

II. Polymers Derived from Renewable Resources

A number of renewable resources contain polymers that are suitable foruse in an absorbent article (i.e., the polymer is obtained from therenewable resource without intermediates). Suitable extraction and/orpurification steps may be necessary, but no intermediate compound isrequired. Such polymers derived directly from renewable resourcesinclude cellulose (e.g. pulp fibers), starch, chitin, polypeptides,poly(lactic acid), polyhydroxyalkanoates, and the like. These polymersmay be subsequently chemically modified to improve end usecharacteristics (e.g., conversion of cellulose to yield carboxycelluloseor conversion of chitin to yield chitosan). However, in such cases, theresulting polymer is a structural analog of the starting polymer.Polymers derived directly from renewable resources (i.e., with nointermediate compounds) and their derivatives are known and thesematerials are not within the scope of the present invention.

The synthetic polymers of the present invention are derived from arenewable resource via an indirect route involving one or moreintermediate compounds. Suitable intermediate compounds derived fromrenewable resources include sugars. Suitable sugars includemonosaccharides, disaccharides, trisaccharides, and oligosaccharides.Sugars such as sucrose, glucose, fructose, maltose may be readilyproduced from renewable resources such as sugar cane and sugar beets.Sugars may also be derived (e.g., via enzymatic cleavage) from otheragricultural products such as starch or cellulose. For example, glucosemay be prepared on a commercial scale by enzymatic hydrolysis of cornstarch. While corn is a renewable resource in North America, othercommon agricultural crops may be used as the base starch for conversioninto glucose. Wheat, buckwheat, arracaha, potato, barley, kudzu,cassava, sorghum, sweet potato, yam, arrowroot, sago, and other likestarchy fruit, seeds, or tubers are may also be used in the preparationof glucose.

Other suitable intermediate compounds derived from renewable resourcesinclude monofunctional alcohols such as methanol or ethanol andpolyfunctional alcohols such as glycerol. Ethanol may be derived frommany of the same renewable resources as glucose. For example, cornstarchmay be enzymatically hydrolysized to yield glucose and/or other sugars.The resultant sugars can be converted into ethanol by fermentation. Aswith glucose production, corn is an ideal renewable resource in NorthAmerica; however, other crops may be substituted. Methanol may beproduced from fermentation of biomass. Glycerol is commonly derived viahydrolysis of triglycerides present in natural fats or oils, which maybe obtained from renewable resources such as animals or plants.

Other intermediate compounds derived from renewable resources includeorganic acids (e.g., citric acid, lactic acid, alginic acid, amino acidsetc.), aldehydes (e.g., acetaldehyde), and esters (e.g., cetylpalmitate, methyl stearate, methyl oleate, etc.).

Additional intermediate compounds such as methane and carbon monoxidemay also be derived from renewable resources by fermentation and/oroxidation processes.

Intermediate compounds derived from renewable resources may be convertedinto polymers (e.g., glycerol to polyglycerol) or they may be convertedinto other intermediate compounds in a reaction pathway which ultimatelyleads to a polymer useful in an absorbent article. An intermediatecompound may be capable of producing more than one secondaryintermediate compound. Similarly, a specific intermediate compound maybe derived from a number of different precursors, depending upon thereaction pathways utilized.

Particularly desirable intermediates include (meth)acrylic acids andtheir esters and salts; and olefins. In particular embodiments, theintermediate compound may be acrylic acid, ethylene, or propylene.

For example, acrylic acid is a monomeric compound that may be derivedfrom renewable resources via a number of suitable routes. Examples ofsuch routes are provided below.

Glycerol derived from a renewable resource (e.g., via hydrolysis ofsoybean oil and other triglyceride oils) may be converted into acrylicacid according to a two-step process. In a first step, the glycerol maybe dehydrated to yield acrolein. A particularly suitable conversionprocess involves subjecting glycerol in a gaseous state to an acidicsolid catalyst such as H₃PO₄ on an aluminum oxide carrier (which isoften referred to as solid phosphoric acid) to yield acrolien. Specificsrelating to dehydration of glycerol to yield acrolein are disclosed, forinstance, in U.S. Pat. Nos. 2,042,224 and 5,387,720. In a second step,the acrolein is oxidized to form acrylic acid. A particularly suitableprocess involves a gas phase interaction of acrolein and oxygen in thepresence of a metal oxide catalyst. A molybdenum and vanadium oxidecatalyst may be used. Specifics relating to oxidation of acrolein toyield acrylic acid are disclosed, for instance, in U.S. Pat. No.4,092,354.

Glucose derived from a renewable resource (e.g., via enzmatic hydrolysisof corn starch) may be converted into acrylic acid via a two stepprocess with lactic acid as an intermediate product. In the first step,glucose may be biofermented to yield lactic acid. Any suitablemicroorganism capable of fermenting glucose to yield lactic acid may beused including members from the genus Lactobacillus such asLactobacillus lactis as well as those identified in U.S. Pat. Nos.5,464,760 and 5,252,473. In the second step, the lactic acid may bedehydrated to produce acrylic acid by use of an acidic dehydrationcatalyst such as an inert metal oxide carrier which has been impregnatedwith a phosphate salt. This acidic dehydration catalyzed method isdescribed in further detail in U.S. Pat. No. 4,729,978. In an alternatesuitable second step, the lactic acid may be converted to acrylic acidby reaction with a catalyst comprising solid aluminum phosphate. Thiscatalyzed dehydration method is described in further detail in U.S. Pat.No. 4,786,756.

Another suitable reaction pathway for converting glucose into acrylicacid involves a two step process with 3-hydroxypropionic acid as anintermediate compound. In the first step, glucose may be biofermented toyield 3-hydroxypropionic acid. Microorganisms capable of fermentingglucose to yield 3-hydroxypropionic acid have been geneticallyengineered to express the requisite enzymes for the conversion. Forexample, a recombinant microorganism expressing the dhaB gene fromKlebsiella pneumoniae and the gene for an aldehyde dehydrogenase hasbeen shown to be capable of converting glucose to 3-hydroxypropionicacid. Specifics regarding the production of the recombinant organism maybe found in U.S. Pat. No. 6,852,517. In the second step, the3-hydroxypropionic acid may be dehydrated to produce acrylic acid.

Glucose derived from a renewable resource (e.g., via enzymatichydrolysis of corn starch obtained from the renewable resource of corn)may be converted into acrylic acid by a multistep reaction pathway.Glucose may be fermented to yield ethanol. Ethanol may be dehydrated toyield ethylene. At this point, ethylene may be polymerized to formpolyethylene. However, ethylene may be converted into propionaldehyde byhydroformylation of ethylene using carbon monoxide and hydrogen in thepresence of a catalyst such as cobalt octacarbonyl or a rhodium complex.Propan-1-ol may be formed by catalytic hydrogenation of propionaldehydein the presence of a catalyst such as sodium borohydride and lithiumaluminum hydride. Propan-1-ol may be dehydrated in an acid catalyzedreaction to yield propylene. At this point, propylene may be polymerizedto form polypropylene. However, propylene may be converted into acroleinby catalytic vapor phase oxidation. Acrolein may then be catalyticallyoxidized to form acrylic acid in the presence of a molybdenum-vanadiumcatalyst.

While the above reaction pathways yield acrylic acid, a skilled artisanwill appreciate that acrylic acid may be readily converted into an ester(e.g., methyl acrylate, ethyl acrylate, etc.) or salt.

Olefins such as ethylene and propylene may also be derived fromrenewable resources. For example, methanol derived from fermentation ofbiomass may be converted to ethylene and or propylene, which are bothsuitable monomeric compounds, as described in U.S. Pat. Nos. 4,296,266and 4,083,889. Ethanol derived from fermentation of a renewable resourcemay be converted into monomeric compound of ethylene via dehydration asdescribed in U.S. Pat. No. 4,423,270. Similarly, propanol or isopropanolderived from a renewable resource can be dehydrated to yield themonomeric compound of propylene as exemplified in U.S. Pat. No.5,475,183. Propanol is a major constituent of fusel oil, a by-productformed from certain amino acids when potatoes or grains are fermented toproduce ethanol.

Charcoal derived from biomass can be used to create syngas (i.e., CO+H₂)from which hydrocarbons such as ethane and propane can be prepared(Fischer-Tropsch Process). Ethane and propane can be dehydrogenated toyield the monomeric compounds of ethylene and propylene.

III. Exemplary Synthetic Polymers

A. Superabsorbent Polymers—Certain compounds derived from renewableresources may be polymerized to yield suitable synthetic superabsorbentpolymers. For example, acrylic acid derived from soybean oil via theglycerol/acrolein route described above may be polymerized under theappropriate conditions to yield a superabsorbent polymer comprisingpoly(acrylic acid). The absorbent polymers useful in the presentinvention can be formed by any polymerization and/or crosslinkingtechniques capable of achieving the desired properties. Typical methodsfor producing these polymers are described in Reissue U.S. Patent No.32,649 to Brandt et al.; U.S. Pat. Nos. 4,666,983, 4,625,001, 5,408,019;and published German patent application 4,020,780 to Dahmen. Theprocessing (i.e., drying, milling, sieving, etc.) of the resultingsuperabsorbent polymer to yield a usable form is well known in the art.

The polymer may be prepared in the neutralized, partially neutralized,or un-neutralized form. In certain embodiments, the absorbent polymermay be formed from acrylic acid that is from about 50 mole % to about 95mole % neutralized. The absorbent polymer may be prepared using ahomogeneous solution polymerization process, or by multi-phasepolymerization techniques such as inverse emulsion or suspensionpolymerization procedures. The polymerization reaction will generallyoccur in the presence of a relatively small amount of di- orpoly-functional monomers such as N,N′-methylene bisacrylamide,trimethylolpropane triacrylate, ethylene glycol di(meth)acrylate,triallylamine, and methacrylate analogs of the aforementioned acrylates.The di- or poly-functional monomer compounds serve to lightly cross-linkthe polymer chains thereby rendering them water-insoluble, yetwater-swellable.

In certain embodiments, the synthetic superabsorbent polymer comprisingacrylic acid derived from renewable resources may be formed fromstarch-acrylic acid graft copolymers, partially neutralizedstarch-acrylic acid graft copolymers, crosslinked polymers ofpolyacrylic acid, and crosslinked polymers of partially neutralizedpolyacrylic acid. Preparation of these materials is disclosed in U.S.Pat. Nos. 3,661,875; 4,076,663; 4,093,776; 4,666,983; and 4,734,478.

The synthetic superabsorbent polymers particles can besurface-crosslinked after polymerization by reaction with a suitablereactive crosslinking agents. Surface-crosslinking of the initiallyformed superabsorbent polymers particles derived from renewableresources provides superabsorbent polymers having relatively highabsorbent capacity and relatively high permeability to fluid in theswollen state, as described below. A number of processes for introducingsurface crosslinks are disclosed in the art. Suitable methods forsurface crosslinking are disclosed in U.S. Pat. Nos. 4,541,871,4,824,901, 4,789,861, 4,587,308, 4,734,478, and 5,164,459; published PCTapplications WO92/16565, WO90/08789, and WO93/05080; published Germanpatent application 4,020,780 to Dahmen; and published European patentapplication 509,708 to Gartner. Suitable crosslinking agents include di-or poly-functional crosslinking reagents such as di/poly-haloalkanes,di/poly-epoxides, di/poly-acid chlorides, di/poly-tosyl alkanes,di/poly-aldehydes, di/poly-alcohols, and the like.

An important characteristic of the synthetic superabsorbent polymers ofthe present invention is the permeability or flow conductivity of a zoneor layer of the polymer particles when swollen with body fluids. Thispermeability or flow conductivity is defined herein in terms of theSaline Flow Conductivity (SFC) value of the superabsorbent polymer. SFCmeasures the ability of the swollen hydrogel zone or layer to transportor distribute body fluids under usage pressures. It is believed thatwhen a superabsorbent polymer is present at high concentrations in anabsorbent member and then swells to form a hydrogel under usagepressures, the boundaries of the hydrogel come into contact, andinterstitial voids in this high-concentration region become generallybounded by hydrogel. When this occurs, it is believed the permeabilityor flow conductivity properties of this region are generally reflectiveof the permeability or flow conductivity properties of a hydrogel zoneor layer formed from the superabsorbent polymer alone. It is furtherbelieved that increasing the permeability of these swollenhigh-concentration regions to levels that approach or even exceedconventional acquisition/distribution materials, such as wood-pulpfluff, can provide superior fluid handling properties for the absorbentmember and absorbent core, thus decreasing incidents of leakage,especially at high fluid loadings. Higher SFC values also are reflectiveof the ability of the formed hydrogel to acquire body fluids undernormal usage conditions.

The SFC value of the synthetic superabsorbent polymers derived fromrenewable resources useful in the present invention is at least about30×10⁻⁷ cm³ sec/g. In other embodiments, the SFC value of thesuperabsorbent polymers useful in the present invention is at leastabout 50×10⁻⁷ cm³ sec/g. In other embodiments, the SFC value of thesuperabsorbent polymers useful in the present invention is at leastabout 100×10⁻⁷ cm³ sec/g. Typically, these SFC values are in the rangeof from about 30×10⁻⁷ to about 1000×10⁻⁷ cm³ sec/g. However, SFC valuesmay range from about 50×10⁻⁷ to about 500×10⁻⁷ cm³ sec/g or from about50×10⁻⁷ to about 350×10⁻⁷ cm³ sec/g. A method for determining the SFCvalue of the superabsorbent polymers is provided hereafter in the TestMethods Section.

Another important characteristic of the superabsorbent polymers of thepresent invention is their ability to swell against a load. Thiscapacity versus a load is defined in terms of the superabsorbentpolymer's Absorption Against Pressure (AAP) capacity. When asuperabsorbent polymer is incorporated into an absorbent member at highconcentrations, the polymer needs to be capable of absorbing largequantities of body fluids in a reasonable time period under usagepressures. Usage pressures exerted on the superabsorbent polymers usedwithin absorbent article include both mechanical pressures (e.g.,exerted by the weight and motions of a wearer, taping forces, etc.) andcapillary pressures (e.g., resulting from the acquisition component(s)in the absorbent core that temporarily hold fluid before it is absorbedby the superabsorbent polymer).

The AAP capacity of absorbent polymer of the useful in the presentinvention is generally at least about 15 g/g. In certain embodiments,the AAP capacity of absorbent polymer is generally at least about 20g/g. Typically, AAP values range from about 15 to about 25 g/g. However,AAP values may range from about 17 to about 23 g/g or from about 20 toabout 23 g/g. A method for determining the AAP capacity value of theseabsorbent polymers is provided hereafter in the Test Methods Section.

B. Polyolefins—Olefins derived from renewable resources may bepolymerized to yield polyolefins. Ethylene derived from renewableresources may be polymerized under the appropriate conditions to preparepolyethylene having desired characteristics for use in a particularcomponent of an absorbent article or in the packaging for said article.The polyethylene may be high density, medium density, low density, orlinear-low density. Polyethylene and/or polypropylene may be producedvia free-radical polymerization techniques, or by using Ziegler-Nattacatalysis or Metallocene catalysts.

The polyolefin may be processed according to methods known in the artinto a form suitable for the end use of the polymer. Suitable forms forpolyolefins include a film, an apertured film, a microporous film, afiber, a filament, a nonwoven, or a laminate. Suitable nonwoven formsinclude spunbond webs, meltblown webs, and combinations thereof (e.g.,spunbond-meltblown webs (SM), spunbond-meltblown-spunbond webs (SMS),etc.). The polyolefin may comprise mixtures or blends with otherpolymers such as polyolefins derived from petrochemicals. Depending onthe end use and form, the polyolefin may comprise other compounds suchas inorganic compounds, fillers, pigments, dyes, antioxidants,UV-stabilizers, binders, surfactants, wetting agents, and the like. Forexample, a polyolefin film may be impregnated with inorganic compoundsuch as calcium carbonate, titanium dioxide, clays, silicas, zeolites,kaolin, mica, carbon, and mixtures thereof. Such compounds may serve aspore forming agents which, upon straining the film, may improve thebreathability of the film. This process is described further in U.S.Pat. No. 6,605,172. A binder may be used with a polyolefin fibers,filaments, or nonwoven web. A suitable binder is a styrene-butadienelatex binder available under the trade name GENFLO™ 3160 from OMNOVASolutions Inc.; Akron, Ohio. The resulting binder/polyolefin web may beused as an acquisition layer, which may be associated with the absorbentcore. The polyolefin materials and particularly polyolefin fibers,filaments, and nonwoven webs may treated with a surfactant or wettingagent such as Irgasurf™ available from Ciba Specialty Chemicals ofTarrytown, N.Y.

Polyolefin nonwovens useful in an absorbent article may have a basisweight between about 1 g/m² and about 50 g/m² or between about 5 g/m²and about 30 g/m², as measured according to the Basis Weight Testprovided below. Polyolefin nonwovens suitable for use as a topsheet mayhave an average liquid strike-through time of less than about 4 seconds,as measured according to the Liquid Strike-Through Test provided below.In other embodiments the polyolefin nonwoven may have an averagestrike-through time of less than about 3 seconds or less than about 2seconds.

Polyolefin nonwoven useful as a barrier leg cuff may have a hydrohead ofgreater than about 5 mbar or about 6 mbar and less than about 10 mbar orabout 8 mbar, as measured according to the Hydrohead test providedbelow.

Polyolefin films suitable for use as a backsheet may have an MD tensilestrength of greater than about 0.5 N/cm or about 1 N/cm and less thanabout 6 N/cm or about 5 N/cm, as measured according to the Tensile Testas provided below. For breathable polyolefin films suitable for use as abacksheet, the film may have a Moisture Vapor Transmission Rate (MVTR)of at least about 2000 g/m²/hr, preferably greater than about 2400g/m²/hr, and even more preferably, greater than about 3000 g/m²/hr, asmeasured by the Moisture Vapor Transmission Rate test provided below. Itshould be recognized that non-breathable backsheets, which are alsouseful in diapers, would exhibit an MVTR value of about 0 g/m²/hr.

C. Other Polymers—It should be recognized that any of the aforementionedsynthetic polymers may be formed by using a combination of monomersderived from renewable resources and monomers derived from non-renewable(e.g., petroleum) resources. For example, the superabsorbent polymer ofpoly(acrylic acid) may be polymerized from a combination of acrylic acidderived form renewable resources and acrylic acid derived fromnon-renewable resources. The monomer derived from a renewable resourcemay comprise at least about 5% by weight [weight of renewable resourcemonomer/weight of resulting polymer×100], at least about 10% by weight,at least about 20% by weight, at least about 30% by weight, at leastabout 40% by weight, or at least about 50% by weight of thesuperabsorbent polymer.

IV. Absorbent Articles Comprising the Synthetic Polymer Derived fromRenewable Resources

The present invention relates to an absorbent article comprising asynthetic polymer derived from a renewable resource. The polymer hasspecific performance characteristics. The polymers derived from arenewable resource may be in any suitable form such as a film, nonwoven,superabsorbent, and the like.

FIG. 1A is a plan view of an exemplary, non-limiting embodiment of anabsorbent article in the form of a diaper 20 in a flat, uncontractedstate (i.e., without elastic induced contraction). The garment-facingsurface 120 of the diaper 20 is facing the viewer and the body-facingsurface 130 is opposite the viewer. The diaper 20 includes alongitudinal centerline 100 and a lateral centerline 110. FIG. 1B is across-sectional view of the diaper 20 of FIG. 1A taken along the lateralcenterline 110. The diaper 20 may comprise a chassis 22. The diaper 20and chassis 22 are shown to have a front waist region 36, a rear waistregion 38 opposed to the front waist region 36, and a crotch region 37located between the front waist region 36 and the rear waist region 38.The waist regions 36 and 38 generally comprise those portions of thediaper 20 which, when worn, encircle the waist of the wearer. The waistregions 36 and 38 may include elastic elements such that they gatherabout the waist of the wearer to provide improved fit and containment.The crotch region 37 is that portion of the diaper 20 which, when thediaper 20 is worn, is generally positioned between the legs of thewearer.

The outer periphery of diaper 20 and/or chassis 22 is defined bylongitudinal edges 12 and lateral edges 14. The chassis 22 may haveopposing longitudinal edges 12 that are oriented generally parallel tothe longitudinal centerline 100. However, for better fit, longitudinaledges 12 may be curved or angled to produce, for example, an “hourglass”shape diaper when viewed in a plan view. The chassis 22 may haveopposing lateral edges 14 that are oriented generally parallel to thelateral centerline 110.

The chassis 22 may comprises a liquid permeable topsheet 24, a backsheet26, and an absorbent core 28 between the topsheet 24 and the backsheet26. The absorbent core 28 may have a body-facing surface and a garmentfacing-surface. The topsheet 24 may be joined to the core 28 and/or thebacksheet 26. The backsheet 26 may be joined to the core 28 and/or thetopsheet 24. It should be recognized that other structures, elements, orsubstrates may be positioned between the core 28 and the topsheet 24and/or backsheet 26. In certain embodiments, the chassis 22 comprisesthe main structure of the diaper 20 and other features may added to formthe composite diaper structure. The topsheet 24, the backsheet 26, andthe absorbent core 28 may be assembled in a variety of well-knownconfigurations as described generally in U.S. Pat. Nos. 3,860,003;5,151,092; 5,221,274; 5,554,145; 5,569,234; 5,580,411; and 6,004,306.

The absorbent core 28 may comprise the superabsorbent polymer derivedfrom a renewable resource of the present invention as well as a widevariety of other liquid-absorbent materials commonly used in diapers andother absorbent articles. Examples of suitable absorbent materialsinclude comminuted wood pulp, which is generally referred to as airfelt; chemically stiffened, modified or cross-linked cellulosic fibers;superabsorbent polymers or absorbent gelling materials; melt blownpolymers, including co-form, biosoluble vitreous microfibers; tissue,including tissue wraps and tissue laminates; absorbent foams; absorbentsponges; and any other known absorbent material or combinations ofmaterials. Exemplary absorbent structures for use as the absorbent core28 are described in U.S. Pat. Nos. 4,610,678; 4,673,402; 4,834,735;4,888,231; 5,137,537; 5,147,345; 5,342,338; 5,260,345; 5,387,207;5,397,316; 5,625,222; and 6,932,800. Further exemplary absorbentstructures may include non-removable absorbent core components andremovable absorbent core components. Such structures are described inU.S. Publication 2004/0039361A1; 2004/0024379A1; 2004/0030314A1;2003/0199844A1; and 2005/0228356A1. Ideally, the absorbent core 28 maybe comprised entirely of materials derived from renewable resources;however, the absorbent core 28 may comprise materials derived fromnon-renewable resources.

The absorbent core 28 may comprise a fluid acquisition component, afluid distribution component, and a fluid storage component. A suitableabsorbent core 28 comprising an acquisition layer, a distribution layer,and a storage layer is described in U.S. Pat. No. 6,590,136.

Another suitable absorbent core construction where the superabsorbentpolymer of the present invention may be used is described in U.S.Publication No. 2004/0167486 to Busam et al. The absorbent core of theaforementioned publication uses no or, in the alternative, minimalamounts of absorbent fibrous material within the core. Generally, theabsorbent core may include no more than about 20% weight percent ofabsorbent fibrous material (i.e., [weight of fibrous material/totalweight of the absorbent core]×100).

The topsheet 24 is generally a portion of the diaper 20 that may bepositioned at least in partial contact or close proximity to a wearer.Suitable topsheets 24 may be manufactured from a wide range of materialssuch as woven or nonwoven webs of natural fibers (e.g., wood or cottonfibers), synthetic fibers (e.g., polyester or polypropylene fibers), ora combination of natural and synthetic fibers; apertured plastic films;porous foams or reticulated foams. The topsheet 24 is generally supple,soft feeling, and non-irritating to a wearer's skin. Generally, at leasta portion of the topsheet 24 is liquid pervious, permitting liquid toreadily penetrate through the thickness of the topsheet 24. Suitably,the topsheet 24 comprises a polymer (e.g. polyethylene) derived from arenewable resource. Alternately, a suitable topsheet 24 is availablefrom BBA Fiberweb, Brentwood, Tenn. as supplier code 055SLPV09U.

Any portion of the topsheet 24 may be coated with a lotion as is knownin the art. Examples of suitable lotions include those described in U.S.Pat. Nos. 5,607,760; 5,609,587; 5,635,191; and 5,643,588. The topsheet24 may be fully or partially elasticized or may be foreshortened so asto provide a void space between the topsheet 24 and the core 28.Exemplary structures including elasticized or foreshortened topsheetsare described in more detail in U.S. Pat. Nos. 4,892,536; 4,990,147;5,037,416; and 5,269,775.

The backsheet 26 is generally positioned such that it may be at least aportion of the garment-facing surface 120 of the diaper 20. Backsheet 26may be designed to prevent the exudates absorbed by and contained withinthe diaper 20 from soiling articles that may contact the diaper 20, suchas bed sheets and undergarments. In certain embodiments, the backsheet26 is substantially water-impermeable; however, the backsheet 26 may bemade breathable so as to permit vapors to escape while preventing liquidexudates from escaping. The polyethylene film may be made breathable byinclusion of inorganic particulate material and subsequent tensioning ofthe film. Breathable backsheets may include materials such as wovenwebs, nonwoven webs, composite materials such as film-coated nonwovenwebs, and microporous films. Suitably, the backsheet 26 comprises apolymer such (e.g. polyethylene) derived from a renewable resource asdisclosed above. Alternative backsheets 26 derived from non-renewableresources include films manufactured by Tredegar Industries Inc. ofTerre Haute, Ind. and sold under the trade names X15306, X10962, andX10964; and microporous films such as manufactured by Mitsui Toatsu Co.,of Japan under the designation ESPOIR NO and by EXXON Chemical Co., ofBay City, Tex., under the designation EXXAIRE. Other alternativebreathable backsheets 26 are described in U.S. Pat. Nos. 5,865,823,5,571,096, and 6,107,537.

Backsheet 26 may also consist of more than one layer. For example, thebacksheet 26 may comprise an outer cover and an inner layer or maycomprise two outer layers with an inner layer disposed therebetween. Theouter cover may have longitudinal edges and the inner layer may havelongitudinal edges. The outer cover may be made of a soft, non-wovenmaterial. The inner layer may be made of a substantiallywater-impermeable film. The outer cover and an inner layer may be joinedtogether by adhesive or any other suitable material or method. Suitably,the nonwoven outer cover and the water-impermeable film comprisepolymers (e.g., polyethylene) may be derived from renewable resources.Alternatively, a suitable outer cover and inner layer derived fromnon-renewable resources are available, respectively, as supplier codeA18AH0 from Corovin GmbH, Peine, Germany and as supplier code PGBR4WPRfrom RKW Gronau GmbH, Gronau, Germany. While a variety of backsheetconfigurations are contemplated herein, it would be obvious to thoseskilled in the art that various other changes and modifications can bemade without departing from the spirit and scope of the invention.

The diaper 20 may include a fastening system 50. When fastened, thefastening system 50 interconnects the front waist region 36 and the rearwaist region 38. When fastened, the diaper 20 contains a circumscribingwaist opening and two circumscribing leg openings. The fastening system50 may comprise an engaging member 52 and a receiving member 54. Theengaging member 52 may comprise hooks, loops, an adhesive, a cohesive, atab, or other fastening mechanism. The receiving member 54 may comprisehooks, loops, a slot, an adhesive, a cohesive, or other fasteningmechanism that can receive the engaging member 52. Suitable engagingmember 52 and receiving member 54 combinations are well known in the artand include but are not limited to hooks/loop, hooks/hooks,adhesive/polymeric film, cohesive/cohesive, adhesive/adhesive, tab/slot,and button/button hole. Suitably, the fastening system 50 may comprise apolymer (e.g., polyethylene film or a polyethylene nonwoven) derivedfrom a renewable resource.

The diaper 20 may include front ears (not shown) and/or back ears 42.The front and/or back ears 42 may be unitary elements of the diaper 20(i.e., they are not separately manipulative elements secured to thediaper 20, but rather are formed from and are extensions of one or moreof the various layers of the diaper). In certain embodiments, the frontand/or back ears 42 may be discrete elements that are joined to thechassis 22, as shown in FIG. 1A. Discrete front and/or back ears 42 maybe joined to the chassis 22 by any bonding method known in the art suchas adhesive bonding, pressure bonding, heat bonding, and the like. Inother embodiments, the front and/or back ears 42 may comprise a discreteelement joined to the chassis 22 with the chassis 22 having a layer,element, or substrate that extends over the front and/or back ear 42.The front ears and back ears 42 may be extensible, inextensible,elastic, or inelastic. The front ears and back ears 42 may be formedfrom nonwoven webs, woven webs, knitted fabrics, polymeric andelastomeric films, apertured films, sponges, foams, scrims, andcombinations and laminates thereof. In certain embodiments the frontears and back ears 42 may be formed of a stretch laminate comprising afirst nonwoven 42 a, elastomeric material 42 b, and, optionally, asecond nonwoven 42 c or other like laminates. The first and secondnonwoven 42 a, 42 c may comprise a synthetic polymer (e.g.,polyethylene) derived from a renewable resource. A suitable elastomericmaterial 42 b may comprise a natural elastomer such as natural rubber ormay comprise a synthetic elastomer such as the elastomeric filmavailable from Tredegar Corp, Richmond, Va., as supplier code X25007. Analternate stretch laminate may be formed from the Tredegar X25007elastomer disposed between two nonwoven layers (available from BBAFiberweb, Brentwood, Tenn. as supplier code FPN332).

The diaper 20 may further include leg cuffs 32 a, 32 b which provideimproved containment of liquids and other body exudates. Leg cuffs 32 a,32 b may also be referred to as gasketing cuffs, outer leg cuffs, legbands, side flaps, elastic cuffs, barrier cuffs, second cuffs, inner legcuffs, or “stand-up” elasticized flaps. U.S. Pat. No. 3,860,003describes a disposable diaper which provides a contractible leg openinghaving a side flap and one or more elastic members to provide anelasticized leg cuff (i.e., a gasketing cuff). U.S. Pat. Nos. 4,808,178and 4,909,803 describe disposable diapers having “stand-up” elasticizedflaps (i.e., barrier cuffs) which improve the containment of the legregions. U.S. Pat. Nos. 4,695,278 and 4,795,454 describe disposablediapers having dual cuffs, including gasketing cuffs and barrier cuffs.

FIGS. 1A-B shows the diaper 20 having dual cuffs: gasketing cuff 32 aand barrier cuff 32 b. The barrier cuff 32 b may include one or morebarrier elastic members 33 b. The barrier elastic members 33 b may bejoined to a barrier cuff substrate 34. The barrier cuff substrate 34 maycomprise a polymer derived from a renewable resource. In certainembodiments, the barrier cuff substrate 34 may be a polymeric film ornonwoven. The barrier cuff 32 b may be disposed on the body-facingsurface of the chassis 22. The barrier cuff substrate 34 may extendlaterally from the longitudinal edge 12 of the chassis 22 to a pointinboard of the longitudinal edge 122. The barrier cuff 32 b generallyextends longitudinally at least through the crotch region 37. Thebarrier elastic members 33 b allow a portion of the barrier cuff 32 b tobe spaced away from the body-facing surface of the diaper 20.

The gasketing cuff 32 a may include one or more gasketing elasticmembers 33 a. The gasketing elastic member 33 a may be joined to one ormore of the existing elements or substrates of the diaper 20 (e.g.,topsheet 24, backsheet 26, barrier cuff substrate 34, etc.). In someembodiments, it may be desirable to treat all or a portion of the legcuffs 32 with a hydrophilic surface coasting such as is described inU.S. Patent Publication 2005/0177123A1. Suitable gasketing and barrierelastic members 33 a, 33 b include natural rubber, synthetic rubbers,and other elastomers.

In other suitable embodiments, the diaper 20 may be preformed by themanufacturer to create a pant. A pant may be preformed by any suitabletechnique including, but not limited to, joining together portions ofthe article using refastenable and/or non-refastenable bonds (e.g.,seam, weld, adhesive, cohesive bond, fastener, etc.). For example, thediaper 20 of FIG. 1A may be manufactured with the fastening system 50engaged (i.e., the engaging member 52 is joined to the receiving member54). As an additional example, the diaper 20 of FIG. 1A may bemanufactured with the front ears 40 joined to the back ears 42 by way ofa bond such as an adhesive bond, a mechanical bond, or some otherbonding technique known in the art. Suitable pants are disclosed in U.S.Pat. Nos. 5,246,433; 5,569,234; 6,120,487; 6,120,489; 4,940,464;5,092,861; 5,897,545; and 5,957,908.

V. Providing the Absorbent Article to a Consumer

One or more absorbent articles (e.g., diapers) 220 may be provided as apackage 200, as shown in FIGS. 2A-B. Generally, the package 200 allowsfor a quantity of absorbent articles 220 to be delivered to andpurchased by a consumer while economizing space and simplifyingtransport and storage. The package 200 includes at least one absorbentarticle 220 secured by an overwrap 250. The overwrap 250 may partiallyor fully cover the absorbent article(s), which may be compressed oruncompressed. FIG. 2A depicts an overwrap 250 that completely covers andencases a plurality of absorbent articles 220. The overwrap 250 maycomprise a variety of materials including, but not limited to,thermoplastic films, nonwovens, wovens, foils, fabrics, papers,cardboard, elastics, cords, straps, and combinations thereof. Othersuitable package structures and overwraps are described in U.S. Pat.Nos. 4,846,587; 4,934,535; 4,966,286; 5,036,978; 5,050,742; and5,054,619. In certain embodiments, the overwrap 250 comprises asynthetic polymer (e.g., a polyolefin) derived form a renewableresource. While the package 200 is not limited in shape, it may bedesirable for the package 200 to have the shape of a parallelepiped orsubstantially similar to a parallelepiped (e.g., a solid at least asubstantially planar base and four substantially planar sides). Such ashape is ideal for packaging, stacking, and transport. The package 200is not limited in size; however, in certain embodiments, the size of thepackage 200 should be no greater than is required to contain theabsorbent articles 220.

The package 200 may have a handle 240. In certain embodiments, thehandle 240 may be a discrete element such as a strap that may be affixedto the overwrap 250. In the embodiment shown in FIGS. 2A-B, the handle240 is integral to the overwrap 250. For this embodiment, the handle 240may comprise an extension 252 from the overwrap 250. The extension 252may have an aperture 254 there through. The aperture 254 ideally sizedto permit entry by one or more digits of an adult hand.

An opening device 260 may be provided in the overwrap 250. For example,the opening device 260 may comprise a line of weakness 262 (e.g.,perforations) in an overwrap 250 made from paper, cardboard, or film.The opening device 260 allows for partial or full removal of a flap 256which is a portion of the overwrap 250. Partial of full removal of theflap 256 may allow for improved access to the absorbent articles 220.The opening device 260 and flap 256 are shown in a closed configurationin FIG. 2A and in an open configuration in FIG. 2B. An exemplary openingdevice 260 is presented in U.S. Pat. No. 5,036,978.

The package 200 may contain multiple overwraps 250. For example, aplurality of absorbent articles may be secured with a first overwrapsuch as a thermoplastic film and then a plurality of film wrappedabsorbent articles may be secured in a second overwrap such as acardboard box or another thermoplastic film.

VI. Communicating a Related Environmental Message a Consumer

The present invention may further comprise a related environmentalmessage or may further comprise a step of communicating a relatedenvironmental message to a consumer. The related environmental messagemay convey the benefits or advantages of the absorbent articlecomprising a polymer derived from a renewable resource. The relatedenvironmental message may identify the absorbent articles as: beingenvironmentally friendly or Earth friendly; having reduced petroleum (oroil) dependence or content; having reduced foreign petroleum (or oil)dependence or content; having reduced petrochemicals or havingcomponents that are petrochemical free; and/or being made from renewableresources or having components made from renewable resources. Thiscommunication is of importance to consumers that may have an aversion topetrochemical use (e.g., consumers concerned about depletion of naturalresources or consumers who find petrochemical based products unnaturalor not environmentally friendly) and to consumers that areenvironmentally conscious. Without such a communication, the benefit ofthe present invention may be lost on some consumers.

The communication may be effected in a variety of communication forms.Suitable communication forms include store displays, posters, billboard,computer programs, brochures, package literature, shelf information,videos, advertisements, internet web sites, pictograms, iconography, orany other suitable form of communication. The information could beavailable at stores, on television, in a computer-accessible form, inadvertisements, or any other appropriate venue. Ideally, multiplecommunication forms may be employed to disseminate the relatedenvironmental message.

The communication may be written, spoken, or delivered by way of one ormore pictures, graphics, or icons. For example, a television or internetbased-advertisement may have narration, a voice-over, or other audibleconveyance of the related environmental message. Likewise, the relatedenvironmental message may be conveyed in a written form using any of thesuitable communication forms listed above. In certain embodiments, itmay be desirable to quantify the reduction of petrochemical usage of thepresent absorbent article compared to absorbent articles that arepresently commercially available.

In other embodiments, the communication form may be one or more icons.FIGS. 3A-F depict several suitable embodiments of a communication in theform of icon 310. One or more icons 310 may be used to convey therelated environmental message of reduced petrochemical usage. Suitableicons 310 communicating the related environmental message of reducedpetroleum usage are shown in FIGS. 3A-B. Icons communicating the relatedenvironmental message of environmental friendliness or renewableresource usage are shown in FIGS. 3C-F. In certain embodiments, theicons 310 may be located on the package 200 (as shown in FIGS. 2A-B)containing the absorbent articles, on the absorbent article, on aninsert adjoining the package or the articles, or in combination with anyof the other forms of the communication listed above.

The related environmental message may also include a message ofpetrochemical equivalence. As presented in the Background, manyrenewable, naturally occurring, or non-petroleum derived polymers havebeen disclosed. However, these polymers often lack the performancecharacteristics that consumers have come to expect when used inabsorbent articles. Therefore, a message of petroleum equivalence may benecessary to educate consumers that the polymers derived from renewableresources, as described above, exhibit equivalent or better performancecharacteristics as compared to petroleum derived polymers. A suitablepetrochemical equivalence message can include comparison to an absorbentarticle that does not have a polymer derived from a renewable resource.For example, a suitable combined message may be, “Diaper Brand A with anenvironmentally friendly absorbent material is just as absorbent asDiaper Brand B.” This message conveys both the related environmentalmessage and the message of petrochemical equivalence.

VII. Method of Making an Absorbent Article Having a Polymer Derived froma Renewable Resource

The present invention further relates to a method for making anabsorbent article comprising a superabsorbent polymer derived from arenewable resource. The method comprises the steps of providing arenewable resource; deriving a monomer from the renewable resource;polymerizing the monomer to form a synthetic superabsorbent polymerhaving a Saline Flow Conductivity value of at least about 30×10⁻⁷cm³·sec/g and an Absorption Against Pressure value of at least about 15g/g; and incorporating said superabsorbent polymer into an absorbentarticle. The present invention further relates to providing one or moreof the absorbent articles to a consumer and communicating reducedpetrochemical usage to the consumer. The polymer derived from renewableresources may undergo additional process steps prior to incorporationinto the absorbent article. Such process steps include drying, sieving,surface crosslinking, and the like.

The present invention further relates to a method for making anabsorbent article comprising a synthetic polyolefin derived from arenewable resource. The method comprises the steps of providing arenewable resource; deriving an olefin monomer from the renewableresource; polymerizing the monomer to form a synthetic polyolefin havinga ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater; and incorporating saidpolyolefin into an absorbent article. The synthetic polyolefin exhibitsone or more of the above referenced performance characteristics. Thepresent invention further relates to providing one or more of theabsorbent articles to a consumer and communicating reduced petrochemicalusage to the consumer. The polymer derived from renewable resources mayundergo additional process steps prior to incorporation into theabsorbent article. Such process steps include, film formation, fiberformation, ring rolling, and the like.

VIII. Validation of Polymers Derived from Renewable Resources

A suitable validation technique is through ¹⁴C analysis. A commonanalysis technique in carbon-14 dating is measuring the ratio of ¹⁴C tototal carbon within a sample (¹⁴C/C). Research has noted that fossilfuels and petrochemicals generally have a ¹⁴C/C ratio of less than about1×10⁻¹⁵. However, polymers derived entirely from renewable resourcestypically have a ¹⁴C/C ratio of about 1.2×10⁻¹². When compared, thepolymers derived from renewable resources may have a ¹⁴C/C ratio threeorders of magnitude (10³=1,000) greater than the ¹⁴C/C ratio of polymersderived from petrochemicals. Polymers useful in the present inventionhave a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater. In other embodiments,the petrochemical equivalent polymers of the present invention may havea ¹⁴C/C ratio of about 1.0×10⁻¹³ or greater or a ¹⁴C/C ratio of about1.0×10⁻¹² or greater. Suitable techniques for ¹⁴C analysis are known inthe art and include accelerator mass spectrometry, liquid scintillationcounting, and isotope mass spectrometry. These techniques are describedin U.S. Pat. Nos. 3,885,155, 4,427,884, 4,973,841, 5,438,194, and5,661,299.

IX. Test Methods

Saline Flow Conductivity

The method to determine the permeability of a swollen hydrogel layer 718is the “Saline Flow Conductivity” also known as “Gel Layer Permeability”and is described in several references, including, EP A 640 330, filedon Dec. 1, 1993, U.S. Ser. No. 11/349,696, filed on Feb. 3, 2004, U.S.Ser. No. 11/347,406, filed on Feb. 3, 2006, U.S. Ser. No. 06/682,483,filed on Sep. 30, 1982, and U.S. Pat. No. 4,469,710, filed on Oct. 14,1982. The equipment used for this method is described below.

Permeability Measurement System

FIG. 4 shows permeability measurement system 400 set-up with theconstant hydrostatic head reservoir 414, open-ended tube for airadmittance 410, stoppered vent for refilling 412, laboratory jack 416,delivery tube 418, stopcock 420, ring stand support 422, receivingvessel 424, balance 426 and piston/cylinder assembly 428.

FIG. 5 shows the piston/cylinder assembly 428 comprising a metal weight512, piston shaft 514, piston head 518, lid 516, and cylinder 520. Thecylinder 520 is made of transparent polycarbonate (e.g., Lexan®) and hasan inner diameter p of 6.00 cm (area=28.27 cm²) with inner cylinderwalls 550 which are smooth. The bottom 548 of the cylinder 520 is facedwith a US. Standard 400 mesh stainless-steel screen cloth (not shown)that is bi-axially stretched to tautness prior to attachment to thebottom 548 of the cylinder 520. The piston shaft 514 is made oftransparent polycarbonate (e.g., Lexan®) and has an overall length q ofapproximately 127 mm A middle portion 526 of the piston shaft 514 has adiameter r of 21.15 mm. An upper portion 528 of the piston shaft 514 hasa diameter s of 15.8 mm, forming a shoulder 524. A lower portion 546 ofthe piston shaft 514 has a diameter t of approximately ⅝ inch and isthreaded to screw firmly into the center hole 618 (see FIG. 6) of thepiston head 518. The piston head 518 is perforated, made of transparentpolycarbonate (e.g., Lexan®), and is also screened with a stretched US.Standard 400 mesh stainless-steel screen cloth (not shown). The weight512 is stainless steel, has a center bore 530, slides onto the upperportion 528 of piston shaft 514 and rests on the shoulder 524. Thecombined weight of the piston head 518, piston shaft 514 and weight 512is 596 g (±6 g), which corresponds to 0.30 psi over the area of thecylinder 520. The combined weight may be adjusted by drilling a blindhole down a central axis 532 of the piston shaft 514 to remove materialand/or provide a cavity to add weight. The cylinder lid 516 has a firstlid opening 534 in its center for vertically aligning the piston shaft514 and a second lid opening 536 near the edge 538 for introducing fluidfrom the constant hydrostatic head reservoir 414 into the cylinder 520.

A first linear index mark (not shown) is scribed radially along theupper surface 552 of the weight 512, the first linear index mark beingtransverse to the central axis 532 of the piston shaft 514. Acorresponding second linear index mark (not shown) is scribed radiallyalong the top surface 560 of the piston shaft 514, the second linearindex mark being transverse to the central axis 532 of the piston shaft514. A corresponding third linear index mark (not shown) is scribedalong the middle portion 526 of the piston shaft 514, the third linearindex mark being parallel with the central axis 532 of the piston shaft514. A corresponding fourth linear index mark (not shown) is scribedradially along the upper surface 540 of the cylinder lid 516, the fourthlinear index mark being transverse to the central axis 532 of the pistonshaft 514. Further, a corresponding fifth linear index mark (not shown)is scribed along a lip 554 of the cylinder lid 516, the fifth linearindex mark being parallel with the central axis 532 of the piston shaft514. A corresponding sixth linear index mark (not shown) is scribedalong the outer cylinder wall 542, the sixth linear index mark beingparallel with the central axis 532 of the piston shaft 514. Alignment ofthe first, second, third, fourth, fifth, and sixth linear index marksallows for the weight 512, piston shaft 514, cylinder lid 516, andcylinder 520 to be re-positioned with the same orientation relative toone another for each measurement.

The cylinder 520 specification details are:

-   -   Outer diameter u of the Cylinder 520: 70.35 mm    -   Inner diameter p of the Cylinder 520: 60.0 mm    -   Height v of the Cylinder 520: 60.5 mm

The cylinder lid 516 specification details are:

-   -   Outer diameter w of cylinder lid 516: 76.05 mm    -   Inner diameter x of cylinder lid 516: 70.5 mm    -   Thickness y of cylinder lid 516 including lip 554: 12.7 mm    -   Thickness z of cylinder lid 516 without lip: 6.35 mm    -   Diameter a of first lid opening 534: 22.25 mm    -   Diameter b of second lid opening 536: 12.7 mm    -   Distance between centers of first and second lid openings 534        and 536: 23.5 mm

The weight 512 specification details are:

-   -   Outer diameter c: 50.0 mm    -   Diameter d of center bore 530: 16.0 mm    -   Height e: 39.0 mm

The piston head 518 specification details are

-   -   Diameter f: 59.7 mm    -   Height g: 16.5 mm    -   Outer holes 614 (14 total) with a 9.65 mm diameter h, outer        holes 614 equally spaced with centers being 47.8 mm from the        center of center hole 618    -   Inner holes 616 (7 total) with a 9.65 mm diameter i, inner holes        616 equally spaced with centers being 26.7 mm from the center of        center hole 618    -   Center hole 618 has a diameter j of ⅝ inches and is threaded to        accept a lower portion 546 of piston shaft 514.

Prior to use, the stainless steel screens (not shown) of the piston head518 and cylinder 520 should be inspected for clogging, holes orover-stretching and replaced when necessary. An SFC apparatus withdamaged screen can deliver erroneous SFC results, and must not be useduntil the screen has been replaced.

A 5.00 cm mark 556 is scribed on the cylinder 520 at a height k of 5.00cm (±0.05 cm) above the screen (not shown) attached to the bottom 548 ofthe cylinder 520. This marks the fluid level to be maintained during theanalysis. Maintenance of correct and constant fluid level (hydrostaticpressure) is critical for measurement accuracy.

A constant hydrostatic head reservoir 414 is used to deliver saltsolution 432 to the cylinder 520 and to maintain the level of saltsolution 432 at a height k of 5.00 cm above the screen (not shown)attached to the bottom 548 of the cylinder 520. The bottom 434 of theair-intake tube 410 is positioned so as to maintain the salt solution432 level in the cylinder 520 at the required 5.00 cm height k duringthe measurement, i.e., bottom 434 of the air tube 410 is inapproximately same plane 438 as the 5.00 cm mark 556 on the cylinder 520as it sits on the support screen (not shown) on the ring stand 440 abovethe receiving vessel 424. Proper height alignment of the air-intake tube410 and the 5.00 cm mark 556 on the cylinder 520 is critical to theanalysis. A suitable reservoir 414 consists of a jar 430 containing: ahorizontally oriented L-shaped delivery tube 418 for fluid delivery, avertically oriented open-ended tube 410 for admitting air at a fixedheight within the constant hydrostatic head reservoir 414, and astoppered vent 412 for re-filling the constant hydrostatic headreservoir 414. Tube 410 has an internal diameter of xx mm. The deliverytube 418, positioned near the bottom 442 of the constant hydrostatichead reservoir 414, contains a stopcock 420 for starting/stopping thedelivery of salt solution 432. The outlet 444 of the delivery tube 418is dimensioned to be inserted through the second lid opening 536 in thecylinder lid 516, with its end positioned below the surface of the saltsolution 432 in the cylinder 520 (after the 5.00 cm height of the saltsolution 432 is attained in the cylinder 520). The air-intake tube 410is held in place with an o-ring collar (not shown). The constanthydrostatic head reservoir 414 can be positioned on a laboratory jack416 in order to adjust its height relative to that of the cylinder 520.The components of the constant hydrostatic head reservoir 414 are sizedso as to rapidly fill the cylinder 520 to the required height (i.e.,hydrostatic head) and maintain this height for the duration of themeasurement. The constant hydrostatic head reservoir 414 must be capableof delivering salt solution 432 at a flow rate of at least 3 g/sec forat least 10 minutes.

The piston/cylinder assembly 428 is positioned on a 16 mesh rigidstainless steel support screen (not shown) (or equivalent) which issupported on a ring stand 440 or suitable alternative rigid stand. Thissupport screen (not shown) is sufficiently permeable so as to not impedesalt solution 432 flow and rigid enough to support the stainless steelmesh cloth (not shown) preventing stretching. The support screen (notshown) should be flat and level to avoid tilting the piston/cylinderassembly 428 during the test. The salt solution 432 passing through thesupport screen (not shown) is collected in a receiving vessel 424,positioned below (but not supporting) the support screen (not shown).The receiving vessel 424 is positioned on the balance 426 which isaccurate to at least 0.01 g. The digital output of the balance 426 isconnected to a computerized data acquisition system (not shown).

Preparation of Reagents (not Illustrated)

Jayco Synthetic Urine (JSU) 712 (see FIG. 7) is used for a swellingphase (see SFC Procedure below) and 0.118 M Sodium Chloride (NaCl)Solution is used for a flow phase (see SFC Procedure below). Thefollowing preparations are referred to a standard 1 liter volume. Forpreparation of volumes other than 1 liter, all quantities are scaledaccordingly.

JSU: A 1 L volumetric flask is filled with distilled water to 80% of itsvolume, and a magnetic stir bar is placed in the flask. Separately,using a weighing paper or beaker the following amounts of dryingredients are weighed to within ±0.01 g using an analytical balanceand are added quantitatively to the volumetric flask in the same orderas listed below. The solution is stirred on a suitable stir plate untilall the solids are dissolved, the stir bar is removed, and the solutiondiluted to 1 L volume with distilled water. A stir bar is againinserted, and the solution stirred on a stirring plate for a few minutesmore.

Quantities of salts to make 1 liter of Jayco Synthetic Urine:

-   -   Potassium Chloride (KCl) 2.00 g    -   Sodium Sulfate (Na₂SO₄) 2.00 g    -   Ammonium dihydrogen phosphate (NH₄H₂PO₄) 0.85 g    -   Ammonium phosphate, dibasic ((NH₄)₂HPO₄) 0.15 g    -   Calcium Chloride (CaCl₂) 0.19 g—[or hydrated calcium chloride        (CaCl₂·2H₂O) 0.25 g]    -   Magnesium chloride (MgCl₂) 0.23 g—[or hydrated magnesium        chloride (MgCl₂·6H₂O) 0.50 g]

To make the preparation faster, each salt is completely dissolved beforeadding the next one. Jayco synthetic urine may be stored in a cleanglass container for 2 weeks. The solution should not be used if itbecomes cloudy. Shelf life in a clean plastic container is 10 days.

0.118 M Sodium Chloride (NaCl) Solution: 0.118 M Sodium Chloride is usedas salt solution 432. Using a weighing paper or beaker 6.90 g (±0.01 g)of sodium chloride is weighed and quantitatively transferred into a 1 Lvolumetric flask; and the flask is filled to volume with distilledwater. A stir bar is added and the solution is mixed on a stirring plateuntil all the solids are dissolved.

Test Preparation

Using a solid reference cylinder weight (not shown) (40 mm diameter; 140mm height), a caliper gauge (not shown) (e.g., Mitotoyo Digimatic HeightGage) is set to read zero. This operation is conveniently performed on asmooth and level bench top 446. The piston/cylinder assembly 428 withoutsuperabsorbent is positioned under the caliper gauge (not shown) and areading, L₁, is recorded to the nearest 0.01 mm.

The constant hydrostatic head reservoir 414 is filled with salt solution432. The bottom 434 of the air-intake tube 410 is positioned so as tomaintain the top part (not shown) of the liquid meniscus (not shown) inthe cylinder 520 at the 5.00 cm mark 556 during the measurement. Properheight alignment of the air-intake tube 410 at the 5.00 cm mark 556 onthe cylinder 520 is critical to the analysis.

The receiving vessel 424 is placed on the balance 426 and the digitaloutput of the balance 426 is connected to a computerized dataacquisition system (not shown). The ring stand 440 with a 16 mesh rigidstainless steel support screen (not shown) is positioned above thereceiving vessel 424. The 16 mesh screen (not shown) should besufficiently rigid to support the piston/cylinder assembly 428 duringthe measurement. The support screen (not shown) must be flat and level.

SFC Procedure

0.9 g (±0.05 g) of superabsorbent is weighed onto a suitable weighingpaper using an analytical balance. 0.9 g (±0.05 g) of superabsorbent isweighed onto a suitable weighing paper using an analytical balance. Themoisture content of the superabsorbent is measured according to theEdana Moisture Content Test Method 430.1-99 (“Superabsorbentmaterials—Polyacrylate superabsorbent powders—MOISTURE CONTENT—WEIGHTLOSS UPON HEATING” (February 99)). If the moisture content of thepolymer is greater than 5%, then the polymer weight should be correctedfor moisture (i.e., the added polymer should be 0.9 g on a dry-weightbasis).

The empty cylinder 520 is placed on a level benchtop 446 and thesuperabsorbent is quantitatively transferred into the cylinder 520. Thesuperabsorbent particles are evenly dispersed on the screen (not shown)attached to the bottom 548 of the cylinder 520 by gently shaking,rotating, and/or tapping the cylinder 520. It is important to have aneven distribution of particles on the screen (not shown) attached to thebottom 548 of the cylinder 520 to obtain the highest precision result.After the superabsorbent has been evenly distributed on the screen (notshown) attached to the bottom 548 of the cylinder 520 particles must notadhere to the inner cylinder walls 550. The piston shaft 514 is insertedthrough the first lid opening 534, with the lip 554 of the lid 516facing towards the piston head 518. The piston head 518 is carefullyinserted into the cylinder 520 to a depth of a few centimeters. The lid516 is then placed onto the upper rim 544 of the cylinder 520 whiletaking care to keep the piston head 518 away from the superabsorbent.The lid 516 and piston shaft 526 are then carefully rotated so as toalign the third, fourth, fifth, and sixth linear index marks are thenaligned. The piston head 518 (via the piston shaft 514) is then gentlylowered to rest on the dry superabsorbent. The weight 512 is positionedon the upper portion 528 of the piston shaft 514 so that it rests on theshoulder 524 such that the first and second linear index marks arealigned. Proper seating of the lid 516 prevents binding and assures aneven distribution of the weight on the hydrogel layer 718.

Swelling Phase: An 8 cm diameter fritted disc (7 mm thick; e.g.Chemglass Inc. #CG 201-51, coarse porosity) 710 is saturated by addingexcess JSU 712 to the fritted disc 710 until the fritted disc 710 issaturated. The saturated fritted disc 710 is placed in a wideflat-bottomed Petri dish 714 and JSU 712 is added until it reaches thetop surface 716 of the fritted disc 710. The JSU height must not exceedthe height of the fitted disc 710.

The screen (not shown) attached to the bottom 548 of the cylinder 520 iseasily stretched. To prevent stretching, a sideways pressure is appliedon the piston shaft 514, just above the lid 516, with the index fingerwhile grasping the cylinder 520 of the piston/cylinder assembly 428.This “locks” the piston shaft 514 in place against the lid 516 so thatthe piston/cylinder assembly 428 can be lifted without undue force beingexerted on the screen (not shown).

The entire piston/cylinder assembly 428 is lifted in this fashion andplaced on the fritted disc 710 in the Petri dish 714. JSU 712 from thePetri dish 714 passes through the fritted disc 710 and is absorbed bythe superabsorbent polymer (not shown) to form a hydrogel layer 718. TheJSU 712 available in the Petri dish 714 should be enough for all theswelling phase. If needed, more JSU 712 may be added to the Petri dish714 during the hydration period to keep the JSU 712 level at the topsurface 716 of the fritted disc 710. After a period of 60 minutes, thepiston/cylinder assembly 428 is removed from the fritted disc 710,taking care to lock the piston shaft 514 against the lid 516 asdescribed above and ensure the hydrogel layer 718 does not lose JSU 712or take in air during this procedure. The piston/cylinder assembly 428is placed under the caliper gauge (not shown) and a reading, L₂, isrecorded to the nearest 0.01 mm. If the reading changes with time, onlythe initial value is recorded. The thickness of the hydrogel layer 718,L₀ is determined from L₂-L₁ to the nearest 0.1 mm.

The entire piston/cylinder assembly 428 is lifted in this the fashiondescribed above and placed on the support screen (not shown) attached tothe ring stand 440. Care should be taken so that the hydrogel layer 718does not lose JSU 712 or take in air during this procedure. The JSU 712available in the Petri dish 714 should be enough for all the swellingphase. If needed, more JSU 712 may be added to the Petri dish 714 duringthe hydration period to keep the JSU 712 level at the 5.00 cm mark 556.After a period of 60 minutes, the piston/cylinder assembly 428 isremoved, taking care to lock the piston shaft 514 against the lid 516 asdescribed above. The piston/cylinder assembly 428 is placed under thecaliper gauge (not shown) and the caliper (not shown) is measured as L₂to the nearest 0.01 mm. The thickness of the hydrogel layer 718, L₀ isdetermined from L₂-L₁ to the nearest 0.1 mm. If the reading changes withtime, only the initial value is recorded.

The piston/cylinder assembly 428 is transferred to the support screen(not shown) attached to the ring support stand 440 taking care to lockthe piston shaft 514 in place against the lid 516. The constanthydrostatic head reservoir 414 is positioned such that the delivery tube418 is placed through the second lid opening 536. The measurement isinitiated in the following sequence:

-   -   a) The stopcock 420 of the constant hydrostatic head reservoir        410 is opened to permit the salt solution 432 to reach the 5.00        cm mark 556 on the cylinder 520. This salt solution 432 level        should be obtained within 10 seconds of opening the stopcock        420.    -   b) Once 5.00 cm of salt solution 432 is attained, the data        collection program is initiated.        With the aid of a computer (not shown) attached to the balance        426, the quantity of salt solution 432 passing through the        hydrogel layer 718 is recorded at intervals of 20 seconds for a        time period of 10 minutes. At the end of 10 minutes, the        stopcock 420 on the constant hydrostatic head reservoir 410 is        closed. The piston/cylinder assembly 428 is removed immediately,        placed under the caliper gauge (not shown) and a reading, L₃, is        recorded to the nearest 0.01 mm. The final thickness of the        hydrogel layer 718, L_(f) is determined from L₃-L₁ to the        nearest 0.1 mm, as described above. The percent change in        thickness of the hydrogel layer 718 is determined from        (L_(f)/L₀)×100. Generally the change in thickness of the        hydrogel layer 718 is within about ±10%.

The data from 60 seconds to the end of the experiment are used in theSFC calculation. The data collected prior to 60 seconds are not includedin the calculation. The flow rate F_(s) (in g/s) is the slope of alinear least-squares fit to a graph of the weight of salt solution 432collected (in grams) as a function of time (in seconds) from 60 secondsto 600 seconds.

In a separate measurement, the flow rate through the permeabilitymeasurement system 400 (F_(a)) is measured as described above, exceptthat no hydrogel layer 718 is present. If F_(a) is much greater than theflow rate through the permeability measurement system 400 when thehydrogel layer 718 is present, F_(s), then no correction for the flowresistance of the permeability measurement system 400 (including thepiston/cylinder assembly 428) is necessary. In this limit, F_(g)=F_(s),where F_(g) is the contribution of the hydrogel layer 718 to the flowrate of the permeability measurement system 400. However if thisrequirement is not satisfied, then the following correction is used tocalculate the value of F_(g) from the values of F_(s) and F_(a):

F _(g)=(F _(a) ×F _(s))/(F _(a) −F _(s))

The Saline Flow Conductivity (K) of the hydrogel layer 718 is calculatedusing the following equation:

K=[F _(g)(t=0)×L ₀]/[ρ×A×ΔP],

where F_(g) is the flow rate in g/sec determined from regressionanalysis of the flow rate results and any correction due to permeabilitymeasurement system 400 flow resistance, L₀ is the initial thickness ofthe hydrogel layer 718 in cm, ρ is the density of the salt solution 432in gm/cm³. A (from the equation above) is the area of the hydrogel layer718 in cm², ΔP is the hydrostatic pressure in dyne/cm², and the salineflow conductivity, K, is in units of cm³ sec/gm. The average of threedeterminations should be reported.

For hydrogel layers 718 where the flow rate is substantially constant, apermeability coefficient (κ) can be calculated from the saline flowconductivity using the following equation:

κ=Kη

where η is the viscosity of the salt solution 432 in poise and thepermeability coefficient, κ, is in units of cm².

In general, flow rate need not be constant. The time-dependent flow ratethrough the system, F_(S) (t) is determined, in units of g/sec, bydividing the incremental weight of salt solution 432 passing through thepermeability measurement system 400 (in grams) by incremental time (inseconds). Only data collected for times between 60 seconds and 10minutes is used for flow rate calculations. Flow rate results between 60seconds and 10 minutes are used to calculate a value for F_(s) (t=0),the initial flow rate through the hydrogel layer 718. F_(s) (t=0) iscalculated by extrapolating the results of a least-squares fit of F_(S)(t) versus time to t=0.

Absorption Against Pressure

This test measures the amount of a 0.90% saline solution absorbed bysuperabsorbent polymers that are laterally confined in a piston/cylinderassembly under a confining pressure for a period of one hour. EuropeanDisposables and Nonwovens Association (EDANA) test method 442.2-02entitled “Absorption Under Pressure” is used.

Basis Weight

This test measures the mass per unit area for a substrate. EuropeanDisposables and Nonwovens Association (EDANA) test method 40.3-90entitled “Mass Per Unit Area” is used.

Liquid Strike-Through

This test measures the time it takes for a known volume of liquidapplied to the surface of a substrate to pass through the substrate toan underlying absorbent pad. European Disposables and NonwovensAssociation (EDANA) test method 150.4-99 entitled “Liquid Strike-ThroughTime” is used.

Tensile Test

This test measures the peak load exhibited by a substrate. A preferredpiece of equipment to do the test is a tensile tester such as a MTSSynergie100 or a MTS Alliance, fitted with a computer interface andTestworks 4 software, available from MTS Systems Corporation 14000Technology Drive, Eden Prairie, Minn., USA. This instrument measures theConstant Rate of Extension in which the pulling grip moves at a uniformrate and the force measuring mechanism moves a negligible distance (lessthan 0.13 mm) with increasing force. The load cell is selected such thatthe measured loads (e.g., force) of the tested samples will be between10 and 90% of the capacity of the load cell (typically a 25N or 50N loadcell).

A 1×1 inch (2.5×2.5 cm) sample is die-cut from the substrate using ananvil hydraulic press die to cut the film with the die into individualsamples. A minimum of three samples are created which are substantiallyfree of visible defects such as air bubbles, holes, inclusions, andcuts. Each sample must have smooth and substantially defect-free edges.Testing is performed in a conditioned room having a temperature of 23°C. (±1° C.) and a relative humidity of 50% (±2%) for at least 2 hours.Samples are allowed to equilibrate in the conditioned room for at least2 hours prior to testing.

Pneumatic jaws of the tensile tester, fitted with flat 2.54 cm-squarerubber-faced grips, are set to give a gauge length of 2.54 cm. Thesample is loaded with sufficient tension to eliminate observable slack,but less than 0.05N. The sample is extended at a constant crossheadspeed of 25.4 cm/min until the specimen completely breaks. If the samplebreaks at the grip interface or slippage within the grips is detected,then the data is disregarded and the test is repeated with a new sampleand the grip pressure is appropriately adjusted. Samples are run atleast in triplicate to account for film variability.

The resulting tensile force-displacement data are converted tostress-strain curves. Peak load is defined as the maximum stressmeasured as a specimen is taken to break, and is reported in Newtons percentimeter width (as measured parallel to the grips) of the sample. Thepeak load for a given substrate is the average of the respective valuesof each sample from the substrate.

Moisture Vapor Transmission Rate (MVTR) Test

The MVTR test method measures the amount of water vapor that istransmitted through a film under specific temperature and humidity. Thetransmitted vapor is absorbed by CaCl2 desiccant and determinedgravimetrically. Samples are evaluated in triplicate, along with areference film sample of established permeability (e.g., Exxon Exxairemicroporous material #XBF-110W) that is used as a positive control.

This test uses a flanged cup machined from Delrin (McMaster-Carr Catalog#8572K34) and anhydrous CaCl2 (Wako Pure Chemical Industries, Richmond,Va.; Catalog 030-00525).

The height of the cup is 55 mm with an inner diameter of 30 mm and anouter diameter of 45 mm. The cup is fitted with a silicone gasket andlid containing 3 holes for thumb screws to completely seal the cup.

The cup is filled with CaCl₂) to within 1 cm of the top. The cup istapped on the counter 10 times, and the CaCl₂) surface is leveled. Theamount of CaCl₂) is adjusted until the headspace between the filmsurface and the top of the CaCl2 is 1.0 cm. The film is placed on top ofthe cup across the opening (30 mm) and is secured using the siliconegasket, retaining ring, and thumb screws. Properly installed, thespecimen should not be wrinkled or stretched.

The film must completely cover the cup opening, A, which is 0.0007065m².

The sample assembly is weighed with an analytical balance and recordedto ±0.001 g. The assembly is placed in a constant temperature (40±3° C.)and humidity (75±3% RH) chamber for 5.0 hr±5 min. The sample assembly isremoved, covered with Saran Wrap® and is secured with a rubber band. Thesample is equilibrated to room temperature for 30 min, the plastic wrapremoved, and the assembly is reweighed and the weight is recorded to±0.001 g. The absorbed moisture M_(a) is the difference in initial andfinal assembly weights. MVTR, in g/m²/24 hr (g/m²/24 hours), iscalculated as:

${MVTR} = \frac{\left( {M_{a} \times 24} \right)}{\left( {A \times 5\mspace{14mu}{hours}} \right)}$

Replicate results are averaged and rounded to the nearest 100 g/m²/24hr, e.g., 2865 g/m²/24 hours is herein given as 2900 g/m²/24 hours and275 g/m²/24 hours is given as 300 g/m²/24 hours.

HydroheadX. Examples

Example 1—Polyolefin A suitable polyolefin may be created according tothe following method. An exemplary renewable resource is corn. The cornis cleaned and may be degerminated. The corn is milled to produce a finepowder (e.g., cornmeal) suitable for enzymatic treatment. The hydrolysis(e.g., liquification and saccharification) of the corn feedstock toyield fermentable sugars is well known in the agricultural andbiofermentation arts. A suitable preparation pathway is disclosed inU.S. Pat. No. 4,407,955. A slurry of dry milled corn is created byadding water to the milled corn and an aqueous solution of sulfuric acid(98% acid by weight). Sufficient sulfuric acid should be added toprovide a slurry pH of about 1.0 to about 2.5. The slurry is heated toabout 140° C. to about 220° C. and pressurized to at least about 50psig; however, pressures from about 100 psig to about 1,000 psig mayresult in greater conversion of the starch to fermentable sugars. Theslurry is maintained at the aforementioned temperature and pressure fora few seconds up to about 10 minutes. The slurry may be conveyed throughone or more pressure reduction vessels which reduce the pressure andtemperature of hydrolyzed slurry. The slurry is subjected to standardseparation techniques such as by centrifuge to yield a fermentable sugarliquor. The liquor typically has a dextrose equivalent of at least 75.The resulting sugar liquor is fermented according to processes well knowto a skilled artisan using a suitable strain of yeast (e.g., genus ofSaccharomyces). The resulting ethanol may be separated from the aqueoussolution by standard isolation techniques such as evaporation ordistillation.

Ethanol is dehydrated to form ethylene by heating the ethanol with anexcess of concentrated sulfuric acid to a temperature of about 170° C.Ethylene may also be formed by passing ethanol vapor over heatedaluminum oxide powder.

The resulting ethylene is polymerized using any of the well knownpolymerization techniques such as free radical polymerization,Ziegler-Natta polymerization, or metallocene catalyst polymerization.Low density branched polyethylene (LDPE) is often made by free radicalvinyl polymerization. Linear low density polyethylene (LLDPE) is made bya more complicated procedure called Ziegler-Natta polymerization. Theresulting polyethylene or blends thereof may be processed to yield adesired end product such as a film, fiber, or filament.

As an example, a linear low density polyethylene is made bycopolymerizing ethylene with other longer chain olefins to result in apolymer having a density of about 0.915 g/cm³ to about 0.925 g/cm³. A 49grams/meter² (gsm) cast extruded film is made comprising the linear lowdensity polyethylene and about 35% by weight to about 45% by weightcalcium carbonate (available from English China Clay of America, Inc.under the designation Supercoat™). The film may be made porous viaseveral routes. The film may be warmed and elongated to 500% of thefilm's original length using well known elongation methods andmachinery. The resulting microporous film is capable of exhibiting aMVTR of at least 2000 g/m²/24 hours. Alternately, the film may beincrementally stretched according to the method disclosed in U.S. Pat.No. 6,605,172. The resulting microporous film should exhibit a MVTR ofat least 2000 g/m²/24 hours.

A nonwoven spunbond web may be formed according to methods well known inthe art such as evidenced by U.S. Pat. Nos. 4,405,297 and 4,340,563. Theweb is formed to have a basis weight of about 5 gsm to about 35 gsm. Theindividual filaments can have an average denier of about 5 or less. Theindividual filaments may have a variety of cross-sectional shapes. Asuitable cross-sectional shape is a bilobal shape disclosed in U.S. Pat.No. 4,753,834. The resultant nonwoven may be made more hydrophilic byincorporating a surfactant in the nonwoven as described in U.S.Statutory Invention Registration No. H1670. The nonwoven treated to bemore hydrophilic is suitable for use as a topsheet in an absorbentarticle. The nonwoven should exhibit a Liquid Strike-Through Time ofless than about 4 seconds. The resultant nonwoven may be made morehydrophobic by use of a surface coating as described in U.S. PublicationNo. 2005/0177123A1. The nonwoven treated to be more hydrophobic issuitable for use a cuff substrate in an absorbent article. The treatednonwoven should exhibit a hydrohead of at least about 5 mbar.

Example 2—Superabsorbent Polymer

Preparation of Glycerol

Canola oil is obtained by expressing from canola seeds. Approximately27.5 kg of canola oil, 5.3 kg methanol and 400 g sodium methoxide arecharged to a 50 L round-bottomed flask equipped with a heating mantle,thermometer, nitrogen inlet, mechanical stirrer, and reflux condenser. Aglass eduction tube (dip tube) is situated so that liquid can be removedfrom the bottom of the flask by means of a peristaltic pump. The flaskis purged with nitrogen and the mixture in the flask is heated to 65° C.with stirring. The mixture is allowed to reflux for 2.5 hours, then theheat is turned off, agitation is stopped and the mixture allowed tosettle for 20 minutes. The bottom layer is pumped out of the flask andkept for further use (Fraction 1). Approximately 1.4 kg methanol and 230g sodium methoxide are added to the flask, agitation is resumed, and themixture refluxed at 65° C. for another 2 hours. The heat is turned off,approximately 2.8 L of water are added to the flask and the mixture isstirred for 1 minute. The stirrer is turned off and the mixture allowedto settle for 20 minutes. The bottom layer is then pumped out of theflask and kept for further use (Fraction 2). Approximately 1.6 L ofwater is added to the flask, and the mixture is stirred for 1 minute.The stirrer is turned off and the mixture allowed to settle for 20minutes. The bottom layer is then pumped out of the flask and kept forfurther use (Fraction 3). Fractions 1, 2 and 3 are combined in asuitable flask equipped with a magnetic stirrer. The combined fractionsare stirred to form a homogeneous mixture and heated to 82° C. Sodiumhydroxide solution (50%) is added slowly until the pH of the mixture is11-13 and the temperature is maintained at 82° C. for a further 10minutes. The pH is checked and more NaOH solution added if <11. Thesolution is concentrated at 115° C. under a vacuum of approximately 40mm Hg until bubbling ceases (water content <5%). The solution istransferred to a round bottomed flask and the glycerol is vacuumdistilled using a rotary evaporator with the oil bath temperature at170° C. and the condenser at 130-140° C. The vacuum is controlled toachieve a moderate distillation rate. A center cut of distilled glycerolis collected.

Preparation of Acrolien

Approximately 200 g of fused aluminum oxide, 6-12 US standard mesh,primarily α-phase, is mixed with 50 g of a 20% solution of phosphoricacid for one hour. The mixture is dried under vacuum by means of arotary evaporator with the oil bath temperature at 80° C. A stainlesssteel tube (chromatography column) with an internal diameter ofapproximately 15 mm and contour length approximately 60 cm is packedwith the dried particles. The column is installed in a gas chromatograminstrument with the inlet connected to the injector port, and the outletconnected to a condenser and collection vessel. The column and injectorport are heated to 300° C. and a 20% aqueous solution of glycerolderived from canola oil is injected at a rate of 40 mL/h. An inertcarrier gas such as helium is optionally utilized to help transport thevapor through the column. The vapors emanating from the column outletare condensed and collected. Acrolein is isolated from the condensate byfractional distillation or other suitable methods known to those skilledin the art.

Preparation of Acrylic Acid

A Pyrex glass reactor approximately 12 cm×2.5 cm OD equipped with athermowell is packed with 31 g (30 mL bulk volume) of a catalystcontaining 2 wt % palladium and 0.5 wt % copper supported on alumina.The reactor is heated in an oil bath at 152° C. A gaseous streamconsisting of 3.4% acrolien, 14.8% oxygen, 22.9% steam, and 58.5%nitrogen by volume, is passed through the heated catalyst at such a ratethat the superficial contact time was about 5 seconds. The reactionmixture is then passed through two water scrubbers connected in seriesheld at 0° C. The aqueous solutions collected are combined and acrylicacid separated from the mixture by fractional distillation.

Preparation of Superabsorbent Polymer

L-Ascorbic Acid (0.2081 g, 1.18 mmol) is added to a 100 mL volumetricflask and is dissolved in distilled water (approximately 50 mL). Afterapproximately ten minutes the solution is diluted to the 100 mL mark onthe volumetric flask with distilled water and the flask was inverted andagitated to ensure a homogeneous solution.

To a 3 L jacketed resin kettle is added TMPTA (0.261 g, 0.881 mmol),acrylic acid (296.40 g, 4.11 mol), and distilled water (250 g). Water iscirculated through the jacket of the resin kettle by means of acirculating water bath kept at 25° C. To the monomer solution is addedstandard 5N sodium hydroxide solution (576 mL, 2.88 mol). The resinkettle is capped with a lid having several ports. An overhead mechanicalstirrer is set up using an air-tight bushing in the central port. Athermometer is inserted through a seal in another port so that the bulbof the thermometer is immersed in the mixture throughout the reaction.The solution is stirred using the overhead mechanical stirrer and purgedwith nitrogen using a fritted gas dispersion tube for approximatelyfifteen minutes. Nitrogen is vented from the kettle via an 18-gaugesyringe needle inserted through a septum in the lid.

After approximately fifteen minutes the fritted gas dispersion tube israised above the surface of the monomer solution and nitrogen was keptflowing through the headspace of the kettle. A solution of sodiumpersulfate (0.4906 g, 2.06 mmol) in distilled water (5 mL), and then asmall aliquot of the L-ascorbic acid solution (1 mL, 1.18 mmol) is addedvia syringe. The mechanical stirrer is stopped when the vortex in thepolymer solution disappears due to the increase in viscosity of thesolution (a few seconds after adding the L-ascorbic acid solution). Thepolymerization reaction proceeds with the circulating bath at 25° C. for30 minutes. After 30 minutes the temperature of the water bath isincreased to 40° C. and held for an additional 30 minutes. Thetemperature of the water bath is then increased to 50° C. and held foranother hour. The peak temperature of the static polymerization isapproximately 70° C.

After one hour at 50° C. the circulating water bath is turned off. Theresin kettle is opened; the polyacrylate gel is removed and broken intochunks approximately 2 cm in diameter. These are chopped into smallerparticles using a food grinder attachment with 4.6 mm holes on aKitchen-Aid mixer (Proline Model KSM5). Distilled water is addedperiodically from a squirt bottle to the infeed portion of the grinderto facilitate passage of the bulk gel through the grinder. Approximately200 g of distilled water is used for this purpose. The chopped gel isspread into thin layers on two separate polyester mesh screens eachmeasuring approximately 56 cm×48 cm and dried at 150° C. for 90 minutesin a vented oven in a fashion which allows passage of air through themesh.

The dried gel is then milled through a Laboratory Wiley Mill using a20-mesh screen. Care is taken to ensure that the screen does not becomeclogged during the grinding process. The milled dried gel is sieved toobtain a fraction with particles which pass through a No. 20 USAStandard Testing Sieve and are retained on a No. 270 USA StandardTesting Sieve. The ‘on 20’ and ‘through 270’ fractions are discarded.

The resultant free-flowing powder fraction ‘through 20’ and ‘on 270’ isdried under vacuum at room temperature until further use.

A 50% solution of ethylene carbonate (1,3-dioxolan-2-one) is prepared bydissolving 10.0 grams of ethylene carbonate in 10.0 grams of distilledwater.

100.00 grams of the dried ‘through 20’ and ‘on 270’ powder above areadded to a stainless steel mixing bowl (approximately 4 L) of a KitchenAid mixer (Proline Model KSM5) equipped with a stainless steel wirewhisk. The height of the mixing bowl is adjusted until the wire whiskjust contacts the bowl. The whisk is started and adjusted to a speedsetting of ‘6’ to stir the particles Immediately thereafter, 15 grams ofthe above 50 wt % ethylene carbonate solution is added to the stirredAGM via a 10 mL plastic syringe equipped with a four inch 22-gaugeneedle. The solution is added directly onto the stirred particles over aperiod of several seconds. The syringe is weighed before and after theaddition of solution to determine the amount added to the particles.After the solution is added, the mixture is stirred for approximatelythirty seconds to help ensure an even coating. The resultant mixture isquite homogeneous with no obvious large clumps of material or residualdry powder. The mixture is then immediately transferred to a Teflonlined 20 cm×35 cm metal tray, spread into a thin layer and placed into avented oven at 185° C. for one hour.

After one hour, the mixture is removed from the oven and allowed to coolfor approximately one minute. After cooling the powder is placed in a 12cm diameter mortar and any agglomerated pieces are gently broken apartwith a pestle. The resultant powder is sieved to obtain a fraction whichpasses through a No. 20 US standard screen, but is retained on a No. 270US standard screen.

The resultant ‘through 20’ and ‘on 270’ superabsorbent polymer particlesare stored under vacuum at room temperature until further use. The AAPvalue for this material is measured according to the EDANA test method442.2-02, and the SFC value is measured according to the SFC Test Methoddescribed above. The AAP value is found to be about 21 g/g, and the SFCvalue is found to be about 50×10⁻⁷ cm³·sec/g

The dimensions and values disclosed herein are not to be understood asbeing strictly limited to the exact numerical values recited. Instead,unless otherwise specified, each such dimension is intended to mean boththe recited value and a functionally equivalent range surrounding thatvalue. For example, a dimension disclosed as “40 mm” is intended to mean“about 40 mm”.

All documents cited in the Detailed Description of the Invention are, inrelevant part, incorporated herein by reference; the citation of anydocument is not to be construed as an admission that it is prior artwith respect to the present invention. To the extent that any definitionor meaning of a term in this written document conflicts with anydefinition or meaning of the term in a document incorporated byreference, the definition or meaning assigned to the term in thisdocument shall govern.

What is claimed is:
 1. A method for making a polyolefin for use in a disposable absorbent article, the method comprising the steps of: (a) providing a first monomer derived from a renewable resource; (b) providing a second monomer derived from petrochemicals; (c) polymerizing the first monomer and the second monomer to form a polyolefin comprising the first monomer and the second monomer; and (d) extruding the polyolefin to form a film, fibers, or filaments for use in one of more components of a disposable absorbent article.
 2. The method of claim 1, wherein the first monomer comprises at least 5% by weight, defined by: (weight of renewable resource monomer/weight of resulting polymer)×100.
 3. The method of claim 1, wherein the first monomer comprises at least 10% by weight, defined by: (weight of renewable resource monomer/weight of resulting polymer)×100.
 4. The method of claim 1, wherein a nonwoven is formed from the fibers or filaments.
 5. The method of claim 4, wherein the nonwoven comprises a spunbond web.
 6. The method of claim 4, wherein the nonwoven comprises a meltblown web.
 7. The method of claim 4, wherein the nonwoven comprises a spunbond-meltblown web or a spunbond-meltblown-spunbond web.
 8. The method of claim 1, wherein the first monomer derived from the renewable resource is at least partially derived from sugar cane, sugar beets, starch, cellulose, sugars, glycerol, natural fats or oils, biomass, or combinations thereof.
 9. The method of claim 4, wherein the nonwoven has a basis weight of from about 5 g/m² to about 30 g/m².
 10. The method of claim 1, wherein the filaments have an average denier of about 5 or less.
 11. The method of claim 1, wherein the film, fibers, or filaments comprise a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater.
 12. The method of claim 4, wherein the nonwoven comprises a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater.
 13. A method for making a polyolefin for use in a disposable absorbent article, the method comprising the steps of: (a) providing a first monomer derived from a renewable resource, wherein the first monomer derived from the renewable resource is at least partially derived from sugar cane, sugar beets, starch, cellulose, sugars, glycerol, biomass, or combinations thereof; (b) providing a second monomer derived from petrochemicals; (c) polymerizing the first monomer and the second monomer to form a polyolefin comprising the first monomer and the second monomer; and (d) extruding the polyolefin to form a film, fibers, or filaments for use in one of more components of a disposable absorbent article.
 14. The method of claim 13, wherein the first monomer comprises at least 5% by weight, defined by: (weight of renewable resource monomer/weight of resulting polymer)×100.
 15. The method of claim 13, wherein the first monomer comprises at least 10% by weight, defined by: (weight of renewable resource monomer/weight of resulting polymer)×100.
 16. The method of claim 13, wherein a nonwoven is formed from the fibers or filaments.
 17. The method of claim 16, wherein the nonwoven comprises a spunbond web.
 18. The method of claim 16, wherein the nonwoven comprises a meltblown web.
 19. The method of claim 16, wherein the nonwoven comprises a spunbond-meltblown web or a spunbond-meltblown-spunbond web.
 20. The method of claim 16, wherein the nonwoven has a basis weight of from about 5 g/m² to about 30 g/m², and wherein the filaments have an average denier of about 5 or less.
 21. The method of claim 13, wherein the film, fibers, or filaments comprise a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater.
 22. The method of claim 16, wherein the nonwoven comprises a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater.
 23. A method for making a polyolefin for use in a disposable absorbent article, the method comprising the steps of: (a) providing a mixture of a first monomer derived from a renewable resource and a second monomer derived from petrochemicals; (b) polymerizing the mixture to form a polyolefin comprising the first monomer and the second monomer; and (c) extruding the polyolefin to form a film, fibers, or filaments for use in one of more components of a disposable absorbent article.
 24. The method of claim 23, wherein a nonwoven is formed from the fibers or filaments.
 25. The method of claim 23, wherein the film, fibers, or filaments comprise a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater.
 26. The method of claim 24, wherein the nonwoven comprises a ¹⁴C/C ratio of about 1.0×10⁻¹⁴ or greater. 